Bannariamman Onsite

7/29/2019 Bannariamman Onsite

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OBJECTIVES OF THE ON-SITE EMERGENCY PLAN

The objective of the ON-SITE EMERGENCY PLAN is to prepare well in advance

to contain effectively any emergency in the shortest time possible with minimum

loss. The plan aims to make the maximum use of the combined resources of the

plant and the outside services to take fast and effective actions in an emergency in

order to:

Protect the personnel, plant and the environment;

Effect the rescue and treatment of casualties, if any;

Safe-guard other personnel and sections in the premises;

Minimize damage to property and environment;

Initially contain and ultimately bring the incident under control;

Provide authoritative information to the media; and

Preserve the relevant records and equipment for subsequent enquiry.

DEFINITION OF TERMS

Hazard The size and nature of the event foreseen

Risk The probability that the event could occur

Major Emergency An industrial emergency could be defined as an occurrence of

such magnitude so as to create a situation in which normal

pattern of life within an industrial plant is suddenly disrupted,

adversely affecting not only the personnel and property within

such an industrial area, but also in the vicinity. It will require

the assistance from the outside agencies and use of outside

resources to handle it effectively.

Key Personnel The essential actions during an emergency depending upon

the circumstances. Nevertheless, it is imperative that the

required actions are promptly and effectively organized by the

nominated people, each taking specified responsibilities as


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part of coordinated plan. Such nominated personnel are known

as KEY PERSONNEL.

Main Controller The Chief Emergency Controller who assumes absolute

control of the industrial premises and determines the actions

necessary to control the emergency.

Incident Controller Site Incident Controller is the person who goes to the scene of

emergency and directs the actions at the main location of the

incident to overcome the emergency situation.

Emergency The Emergency Control Room is the place from where

Control room the necessary

Control Room actions to handle emergency are directed

and coordinated.

Assembly Point In an Emergency, it will almost certainly be necessary to

evacuate the personnel from the affected areas and as a

precautionary measure, to further evacuate the non-essential

workers from the areas likely to be affected, should the

emergency escalate. The evacuation will be effected on

getting the appropriate message from the Main Controller. On

evacuation, the employees will be directed to pre-determined

safe place called ASSEMBLY POINTS and the Assembly

Points are to be located well away from the plant and

equipment and near the exit from the factory premises. Such

Assembly Points shall be conspicuously displayed.

Escape Route Roads leading to the Assembly Points are termed as the

Escape Routes.

Essential Essential Personnel are those to whom the specific


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Personnel responsibilities are assigned in the management of the On-

Site Emergency .

Non-Essential Non-Essential Personnel are those to whom specific

Personnel responsibility is not assigned in the management of On-Site

Emergency.

AFFF Aqueous Film Forming Foam

AR-AFFF Alcohol Resistant Aqueous Film Forming Foam

Coal Rank The agglomerating value is used to differentiate between Coal

Ranks and also is a guide to determine how a particular Coal

reacts in a furnace; this classification is based of the fixed

carbon, volatile matter and the heating value.

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PROCESS AND ACTIVITIES

SUGARCANE PROCESSING

Growing and Handling

Sugarcane, the raw material for the process, is cultivated and grown in extensive

cane fields on the assigned periphery. The cane from the fields is transported by

trucks or tractors and trailers to the cane yard adjacent to the Sugar Processing

Factory. The cane is weighed and unloaded from the vehicles by c anerab

unloaders. The cane is transferred to the main cane carrier for processing as

required. The raw sugarcane from the cane carrier is first cut down to small pieces

by a series of cutting knives, and then chopped further in the fibrizer, which shreds

the cane and exposes the sugar containing cells.

Milling

At the Milling Section, the cane passes through a series of rollers that crush the

cane extract the juice. The juice flows through the machinery to a metal trough

below the floor and is then pumped to a receiving tank. The Bagasse (waste

sugarcane material) is conveyed to the Boiler Furnaces for burning as fuel. The

objective is to optimize the milling operation, juice drainage, good mill setting and

continuous even grinding rate.

Clarifying

From the receiving tank, batches of cane juices are pumped to the primary juice

heaters, where it is heated to about 65 to 70 Degree Centigrade. The heated cane

juice is then pumped to a reaction tank, where Lime solution is added to prevent

Sucrose inversion by increasing the Ph from 5.2 to 7.8. The Lime solution is

formed by adding powdered Lime (calcium oxide) and water in the slaker.

From the reaction tank, the cane juices are heated in the secondary heaters from

100 to 102 Degree Centigrade and are then pumped to a clarifier, where the solids

are allowed to settle out. The clarifier mud is collected and transported to the

filters, where Bagacillo ( fine bagasse particles) are used as a filter medium to

extract the remaining filtrate from the clarifier mud. The clarifier is cleaned every


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two weeks. The filter cake (dried clarifier mud) from the filters is transported to the

sugarcane fields for use as soil amendment and the filtrate is recycled back into

the cane juice process.


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Evaporating

The clear juice from the clarifier is pumped to the multiple effect evaporators,

where it is concentrated from about 85 % water to 40 % water. The concentrated

juice is now called syrup and the syrup is pumped to the Sulphitor, where Sulphur-

Di-Oxide Gas is bubbled through the syrup. The Sulphur-Di-Oxide Gas is created

in the Sulphur burner by igniting powdered sulphur, which serves three purposes:

It acts as a disinfectant;

Reduces the viscosity of the slurry; and

Bleaches the syrup.

Crystallizi ngAfter bleaching, the syrup is taken to the vacuum pans for the purpose of

crystallization. Molasses is then separated from the sugar in the centrifuge, and

the sugar is discharged to a conveyor that is taken for weighing in

50 /100Kgs. Bags for shipment out for sale or staked.

The molasses is then piped to the above-ground storage tanks, from where it is

transported to the Distillery Division for Alcohol Manufacture. Molasses is having a

flammability rating of 1 and will burn only under conditions of extreme heat. The

auto-ignition temperature of molasses is 60 Degree Centigrade and its boiling

point is 107 Degree Centigrade.

CO-GENERATION PLANT

M/S Sakthi Sugars Limited, Sakthinagar plant burns Coal/Bagasse to drive the

turbo-generators, and for sugar processing in the boiling house. Bagasse quality

(moisture and ash content) is important for boiler efficiency. Bagasse moisture in

the range of 45-48 % is desirable for efficient burning. The Bagasse production is

estimated to about 2100 MT/Day.

DISTILLERY - ALCOHOL MANUFACTURING PROCESS

Sakthi Sugars Ltd M/s. Bannari Amman Sugars Limited, Distillery Division is adoptingcontinuous fermentation system which comprises 5 fermentors. Molasses and


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water are added separately to the first 3 - 4 fermenters in suitable proportion. Yeast

is cultured and added only during initial start up of the fermentation process. Air

is passed into the first two fermentors and carbon-di-oxide in the remaining 3

fermenters. The retention time of fermentation is 22 - 24 hours. The temperature of

the fermentors is maintained at 32 - 34 Deg.C. by means of heat exchanger. During

this fermentation period the sugar which is available in the molasses is converted into

alcohol and carbon-di-oxide. Throughout the process, the pH is maintained in the

range of 4 to 5 to control the bacterial contamination. After the fermentation is

completed, the fermented liquid is boiled in the boiling column and alcohol is

concentrated in the rectification column and the finished product namely rectified

spirit is produced and stored in storage tanks.

MANAGING HEALTH AND SAFETY

A number of emergency situations might arise within sugar milling as well as co-

generation and distillery operations including, but not limited to:

(a) Fire and explosion;

(b) Chemical spills;

(c) Rescue from Heights and

(d) Rescue from confined spaces.


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FLOW CHART OF SUGAR PROCESS

+

+

Clear juiceMuddy Juice

Scum Filtrate Juice

Clear Filtrate Juice

Cane 100 % Water 30 %

Juice 100 % Bagasse 30 %

Primary Heating @ 70 o C

Purification

Secondary Heating @ 102 o C

Dorr Clarifier

Vacuum Filter

FilterateFiltrate Clarifier

EvorporatorsEvaporators(Concentration)

Syrup purification

Pans (Crystallization)

Milk of Lime Sulphur-di-oxide Gas

Fuel to Boiler

Press Mud

Centrifugals (separation ofSugar and Molasses)

Sugar

Molasses Distillery

Drier Grader Bagging


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FLOW CHART OF CO-GENERATION PLANT - 32 MW

170 tph, 86 Kg/cm2 , 515oC

HP Heater 9 ATA sugarprocess steam

3 ATA sugar process steam

11 KV

110 KV

BAGASSE / COAL

BOILER

TURBINE

GEAR BOX

ALTERNATOR32 MW / HR

DM WATER

AIR

CHIMNEY

to TNEB

Water cooled condensor

In-house power 5 KW

Condensate

Water cooled condensor


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DETAILS TO BE FURNISHED IN THE ON-SITE EMERGENCY PLAN

1. Name and address of the person furnishing the information:

Thiru. K. RAJENDRAN, KaruppusamyDeputy General Manager - Administration,Sakthi Sugars Limited, Bannari Amman Sugars Limited, distillery

Division ,S.F. No. 272, 273, 274, 276, 280- 283 and 288, Periyapuliyur Post,

Bavani Taluk,Sakthi Nagar P.O., ERODErode District - 638 315455.

2. Personnel of the organization and responsibilities assigned to them incase of an emergency:

i) Thiru. K. Rajendran, Deputy General Manager-

Administration,

Main Site Controller,

ii) Thiru. J. Venkatraman, Assistant General Manager

-HRD,

Alternate Main Site Controller,

iii) Thiru. V. Thiruvenkadam,

Assistant General Manager -Engg.,

Incident Controller ,

iv) Thiru. R. Albert Sam Sukumar,

Deputy General Manager Process

Thiru. K. Sudhakar, Deputy General Manager- Distillery,

Technical Officers,

v) Thiru. S. Nagarajan, Security Officer,

Fire Fighting Officer,vi) Thiru. E. Masanan, Deputy Manager,

Rescue Officer,

vii) Thiru. S. Sesha tdri, Engg. Automobiles,

Rehabilitation Officer,

viii) Thiru. Dr. R. Muthusamy, Chief Medical Officer,

Medical Officer.


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Responsibilities and duties of all the concerned officers in connection with

the On-Site Emergency Plan are enclosed separately for the purpose of

using them during Table-Top Exercises as separate leaf-lets.


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ORGANISATION CHART FOR ONSITE EMERGENCY PLAN

ORGANISATION CHART FORONSITE EMERGENCY PLAN

Main Site RAJENDRAN KController DGM ADMN

Alternate MainCommunicationVENKATARAMAN JSite ControllerOfficer / Alternate A

Technical R. ALBERT SAMSUKUMAROfficer Dy General Manager

ProcessROCESS94433-18805SUDHAKAR KDGM - DISTILLERY

Incident THIRUVENKADAM VController AGM ENGG.

94421-04026

Fire Fighting NAGARAJAN SOfficer SECURITY OFFICER

94421-04040

Rehabilitation SESHADRI SOfficer ENGG. AUTOMOBILES

94431-46384

Rescue MASANAN EOfficer DEPUTY MANAGER

94431-70497

Medical Dr.R. MUTHUSAMYOfficer CHIEF MEDICAL OFFICER

94421-04018

Rehabilitation SESHADRI SOfficer ENGG. AUTOMOBILES

94431-46384

Fire Fighting NAGARAJAN SOfficer SECURITY OFFICER

94421-04040

Technical SUDHAKAR KOfficer DGM -

Medical Dr.R. MUTHUSAMYOfficer CHIEF MEDICALOFFICER

Rescue MASANAN EOfficer DEPUTYMANAGER

Main Site RAJENDRAN KController DGM ADMIN


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3. Outside organizations, if involved, in assisting during onOon-sitteut-sideemergency: i. Type of accidents:

Fire and explosions due to the raw materials such as coalfurnace oil ,

Hydrochloric Acid, Caustic Lye and intermediate product s likebagasse and molasses and Bio-gas .Explosion due to Hydrochloric Acid coming in contact with metallicparts on spillage.Explosion due to Boiler operation

ii. Responsibility Assigned:Tamilnadu Fire and Rescue Service is assigned with theresponsibility of fire fighting and rescue operations in case ofemergency.

4. Details of liaison arrangement between organizations:

Effective coordination and mutual participation in a factory-wide annualtraining has to be established so as to review the On-Site Emergency Planregardless of revisions.

5. Information on the preliminary hazard analysis:

a. Type of accidents :

Fire due to the raw materials such as furnace oil, molasses andBio-gas

Explosion due to Hydrochloric Acid coming in contact with metallicparts on spillage Fire and explosions (coal yard, bagasse yard andturbine areas);

Explosion due to Boiler operation

Toxic and corrosive chemicals (due to D.M. Water TreatmentChemicals such as Hydrochloric Acid and Caustic Lye);

Specific jobs carried under highly hazardous atmosphere (explosiveatmosphere due to Hydrogen evolving from Hydrochloric Acidreacting with metals);

Non-working of safety devices, inter-locks, failure of highly revolvingmachinery . such as steam turbine and centrifugal machines;

Hazards due to handling of heavy equipments ( cranes, trucks,tractors , etc),; and

Traffic hazards.

b. System elements or events that can lead to a majoraccident:

The likely hazards to the factory premises are fire and explosion.

Bagasse, a bye-product of milling process, is normally used as a fuelin Boilers in the Co-Generation Plant in the Sugar Factory which in


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turn produces steam necessary for the factory processes. Bagasse isa natural, fibrous material, which is taken into the atmospheres bywind in respirable sizes. Bagasse is a nuisance dust which is difficultto control, particularly in the form of bagassilo, a dry dust separatedfrom the largest fibers by cyclones and screens, used to mix with

material subsided from juice to create a mill mud. Apart from thehealth risks associated with bagasse fibers, sugar dust and dirt,thermal radiation in case of fire, would be the highest at the center offire and starts falling down as one move away from the seat of fire.

Coal is used as the supplemental fuel in the Boilers of the Co-Generation Plant in the factory. Bituminous Coal is moderatelysubjected to spontaneous heating under the bulk storage conditionsand hence it has to be stored in small piles so as to avoid hightemperatures. High volatile coals are particularly liable to heat asindicated in the National Fire Prevention Association Hand-Book. The

process of slow oxidation of an element/compound, which causes thebulk temperature of the element/compound to rise, without theaddition of an external heat source, is termed as SPONTANEOUSHEATING; it is the result of direct oxidation of hydrocarbons (forexample, oils, coals and solvents) or it may occur because of micro-organisms or organic materials.

Coal presents the hazard between the times it is mined and itseventual use as fuel in Boilers. The oxidation of coal is solid/gasreaction. This happens when the air (a gas) passes over a coalsurface (a solid). Oxygen from the air combines with the coal, raisingthe temperature of the coal. As the reaction proceeds, the moisture inthe coal is liberated as vapor and then some of the volatile matterthat normally has a distinct odor is released. The amount of surfacearea of coal that is exposed is a factor in its heating tendency. Thefiner the size of the coal, the more surface area per unit weight(specific area) and greater the oxidizing potential, all other factorsbeing equal.

c. Hazards:

i. Spontaneous heating:

Coal is stored in the coal storage yard near the Effluent TreatmentArea of the factory premises for use as fuel in the Boilers at therate of 250500 Tons per Day. There is a critical amount of air flowthrough a portion of coal pile that maximizes the oxidation orspontaneous heating tendencies of coal. If there is no air flowthrough a pile, there is no oxygen from the air to stimulateoxidization. If there is potential supply of air, any heat generatedfrom oxidization will be carried off and the pile temperatures reachequilibrium with the air temperature that is considered a ventilated

pile. When there is sufficient air flow for the coal to absorb most ofthe oxygen from the air and an insufficient air flow to dissipate the


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heat generated, the rate of the reaction increases and thetemperature may exceed desirable limits trigger adverse events.

ii. Hydrochloric acid spill:

Apart from the corrosive effects of Hydrochloric Acid, the vaporsfrom the leaky joints, in the course of water treatment activities inthe Co-Generation Plant leads to intense shop-floor corrosion.Hydrochloric Acid on contact with most metals may liberateexplosive and most flammable Hydrogen Gas. During this processof Hydrogen evolution, heat is produced, which, in turn increasesthe generation of vapors of Hydrogen Chloride.

iii. Physical hazards:

The physical hazards include:

Same level fall hazards due to the slippery conditions;

Use of machines and tools;

Collision with internal transport such as trucks and tractorscranes, fork-lifts, conveyors, etc. and

High temperatures and pressures.


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d. d. Safety relevant components:

Attention has to be paid to the correct selection and installation ofgaskets as well as pipe material of construction selected judiciouslyso as to avert any possible flammable and toxic chemical release into

the atmosphere. Necessary procedures have been formulated foravoiding over-pressurization of pipe-lines. Reliability of protectivesystems has been ensured through proper selection, inspection andmaintenance.

The closed coal storage yards (50m x 30m) has been protected with4 Nos. of Hydrants on all the directions. Hence the Hot Spots in thecoal yard could be cooled then and there with constant surveillanceby the security personnel. For the spontaneous ignition to occur, therate of heat being generated through oxidization must exceed therate heat of removal by conduction, convection and radiation

(thermal). As the temperature of the material begins to rise, the rateof heat generation would often increase. The result is a Run-Awayreaction which ultimately causes the ignition. This process ofspontaneous ignition is dependent on the Rank of coals; if the heatremoval exceeds the heat of generation, the coal will cool and will notignite. The rate of heat removal is accomplished through the rotatingof coal piles to cool Hot Spots.

6. Details about the Ssite and e

Location of Dangeroussubstances

Coal

Bituminous Coal is the fuel used in the Boiler of the Co-Generation Plant and thenecessary coal to the tune of 250 Tons per Day is stored in the closed coalstorage yard (50m x 30m) near the Effluent Treatment Area on the southern sideof the factory premises. Bagasse obtained as the bye-product in the MillingProcess at the rate of 2100 Tons per Day is stored in the Bagasse Yard (57m x

41m). Molasses Storage Tank (including 3 Nos. Steel Molasses Tanks) 7 Nos.with a total capacity of 20817 MT as well as 5 Nos. Molasses Tank with a totalcapacity of 19300 MT is located in the Distillery Division and the Sugar Division ofthe Plant. The split-up details of the storage capacity of Molasses in the factory isgiven below:

Division wise molasses storage capacity

a. Distillery division

Sl.No

. Tank No

Capacity in

MT


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1 1 1653.00

2 2 1653.00

3 3 1653.00

4 4 1653.00

5 Steel Tank No.2 6000.006 Steel Tank No.3 6000.00

7 Steel Tank No.4 2205.00

Total

20817.00

b. Sugar divisionc.

Sl.No

.Tank No

Capacity in

MT1 5 3600.00

2 6 3600.00

3 7 4800.00

4 8 3650.00

5 9 3650.00

Total 19300.00

Grand total = (Distillery 20,817 MT + Sugar 19300 MT) = 40,117 MT


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Storage vats capacity in distillery division :

VatNo

Heightin CM

Depth inCM

Capacity inLitres

1. 600 600 1558192 600 600 155831

3 600 600 156108

4 612 612 158600

5 480 480 53052

6 480 480 53147

7 610 610 144207

8 610 610 145011

9 600 600 197492

10 300 300 10600

11 450 450 3273314 994 994 3913976

15 1100 1100 2206759

16 477 477 52164

17 437 437 29528

18 437 437 29528

19 1100 1100 485014

20 1068 1068 2168482

21 1096 1096 482844

Sulphur is stored in the Sulphur Godown to the tune of 900 MT Licensedcapacities. Water Treatment chemicals such as Hydrochloric Acid andCaustic Lye are stored in the D.M.Plant area.

a. Seat of key personnel:

The Deputy General Manager - Administration who is the Main SiteController is normally seated in the Administration Distillery Buildingof the factory will be at the Emergency Control Room in case ofemergency. Emergency Control Room is located near the mainentranceopposite to Boiler plant thein the factory premises and thedetailed On-Site Emergency Plan and Disaster Control Measures asapproved by the Chief Inspector of Factories will be kept readilyavailable in the Emergency Control Room in sufficient numbers forready reference.

b. Emergency Control Room:

The Emergency Control Room is located near the Main Entrancetoopposite to Boiler room in the factory premises and the followinginfra-structural facilities have been made available in the Emergency

Control Room:a) P & T Telephone;


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b) Fax;c) Intercoms;d) Local Area Plans;e) Predominant wind direction and velocity charts;f) Fire Protection System Lay-out Drawings;

g) Emergency Control Numbers List;h) Fire-Suits;i) Breathing Apparatus Set;

j) Face Masks;k) Emergency Lights;l) First-Aid Medicines and accessories;m) White-Board with Marker Pens;n) Sufficient number of gypsum boards; ando) Public Address System.

7. Description of Hazardous Chemicals at the site:

a. Chemicals (Quantities and Toxicological Data:

S. NOHazardous ChemicalsGroup Code Qty. Handled

SUGAR DIVISION :1. Molasses Flammable MT2. Sulphur Flammable MT

DISTILLERY DIVISION:

31. Alcohol Ethanol Flammable - MT2. Molasses Flammable -FUELS USED:

4. Coal Flammable MT/D5. Bagasse Flammable MT/D

D.M. PLANT :

6. Hydrochloric Acid Corrosive MT/M7. Caustic Soda Corrosive MT/M

FUELS USED:

1. Furnace oil Flammable - 3lak lit2. Bio gas Flammable -


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b. Transformation, if any, that could occur:

Below are listed some of the specific characteristics of spontaneousfires in Coalmolasses . These characteristics can be used for the

evaluation of the potential for liquidCoal fire and as guide-lines forminimizing the probability of fires:

a) The higher the inherent (equilibrium moisture), higher theheating tendency;

b) The lower the ash free BTU, the higher the heating tendency,the higher oxygen in the coal, the higher the heatingtendency;

c) Sulphur, once considered as a major factor, is now thought tobe a minor factor, in the spontaneous heating of Coal;

d) The finer the size of the Coal, the more surface area is

exposed per unit weight (specific area) and the greater theoxidizing potential, all other factors being equal;

e) Many times, the segregation of Coal particle sizes are themajor cause of heating. The coarse sizes allow the air toenter into the Coal at one location and react with the highsurface fines at another location;

f) It is generally believed that the rate of reaction is double forevery 8 to 11 Degree Centigrade increase in temperatures;

g) Freshly mined Coal has the greatest oxidizing characteristics,but the Hot Spots in the pile may not appear before one ortwo months; as the initial oxidization takes place, thetemperature gradually increases and the rate of oxidizationaccelerates. There is a critical amount of air flow through aportion of Coal pile, which maximizes oxidization or heatingtendencies of Coal. If there is no air flow through the Coalpile, there is no oxygen from the air to stimulate oxidization. Ifthere is plentiful supply of air, any heat generated throughoxidization will be carried off and the pile temperatures willreach equilibrium with air temperatures, which is consideredas a ventilated pile; and

h) When there is just sufficient air flow for the Coal to absorb

most of the oxygen from the air and an insufficient air flow todissipate the heat generated, the reaction rate increases andthe temperatures may exceed desirable limits.

c. Purity of Hazardous Substances:

Low ash coal contains less than 8 % ash by weight; Low Sulphur coalcontains less than 1 % Sulphur by weight.

8. Likely dangers to the Plant:

The thermal radiation, in case of fire, would be the highest at the center ofthe fire and starts falling down as one move away from the seat of fire.


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Effects of this on human and environment should be known to us tounderstand the damages that can be caused by fire/explosions whilehandling of pulverized Coal as well as Bagasse flammable chemicals in thefactory premise s.s.


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Information available in the Literature is given below:

Heat FluxDamage to Equipment Damage toKW/SQ.M. Human

37.5 Damages to Process Equipment 100% lethality inOne minute; 0.1%In 10 seconds.

25.0 Minimum Energy to ignite wood 100% lethality inindefinitely on long exposure. One minute; signi-

ficant injury in 10seconds.

12.5 Minimum Energy re quired to 1% lethality inIgnite combustion materials minute; 1 Degree

Burns in 10 seconds

9.5 Pain thresholdReached after 10Seconds; II DegreeBurns after 20 sec.

4.0 Causes pain if theduration is longerthan 20 seconds.

1.6 Causes nodiscomfort.

NORMAL CALAMITIES THAT POSES LIKELY DANGERS TO THE PLANT:

Cyclones;

Floods and

Earth Quake.

SOCIETAL RISKS THAT POSES DANGERS TO THE PLANT:

Bomb Threats;

Sabotage and

Arson/Terrorisms, etc.


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9. Enumerate effects of:

(i) Stress and strain caused during normal operation:

Effects of thermal strain have been taken care of by the adequate supply ofgood quality drinking water as well as milk twice a day. Monitoring systemsare in place to ensure that the status of operation is shown clearly at alltimes. These systems include the procedures for a documented hand-overbetween shifts that records any relevant and specific information/changes inthe operating status. Behavior-based observations are duly included in theoperation of equipments and systems handling the hazardous substances.

Any need for additional training is scheduled with these behavior-basedobservations. Strong emphasis has been placed on the training andupgrading of the medical skill of the emergency personnel with the

involvement of Full-Time Medical Officer in the factory, Dr. R.MUTHUSAMY, particularly in their roles as the stress healers for monitoringand management of incident critical stress syndrome, recommending rest,de-briefing or demobilization as required. .

(ii) Fire and explosion inside the plant and effect, if any, of fire andexplosion outside:The inventory of Hazardous Chemicals suggests that the effects of fire andexplosions could be contained within the factory premises and the possibleescalating effects outside the factory premises are remote.

10.DETAILS REGARDING:

i. Warning, alarm, safety and security systems:

Factors that contributed to the significance of emergency includedSystems. A Siren has been provided for in the Sugar factory and the Siren

would be sounded as and when any fire is detected manually by securitypeople during their constant surveillance of the factory premises.

The primary responsibility of informing any emergency situation to theIncident Controller would be religiously followed by the person, who noticesthe fire or Hot Spot in the coal storage yard of in the factory premises. Thefirst responder would be the vocal alerting system through voice audibility,pitch, volume and contents of the message.

In the event of a AlcoholEthanol fire, the flame is less bright than a Gasolineflame and is very faint in bright day-light conditions. Hence the message

that the Ethanol Alcohol Flames what is seen physically are only 5 % ofthe total Fire is conspicuously displayed in the Ethanol Storage Area.


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The plant area has been surrounded by a compound wall and fencing andthe security personnel sufficient in number are deployed for the surveillanceof the factory premises round the clock.

Simple procedures have been devised for those personnel who remainbehind for the critical plant operations; this critical plant shut-down wouldoccur only in the event when there is sudden emergency evacuation orimmediate emergency shelter is not necessary. For the purpose ofminimizing the expected damage from the emergency, the Rescue Officer isassigned with the additional responsibility of shutting them down.

ii. Alarm and Hazard Plan in line with Disaste r Control and Planningensuring the

iii. necessary technical and organizational measures:

The electrical siren will be used for the purpose of Warning andAlarm in the event of an unforeseen emergency.

a) EMERGENCY: Wailing sound for two minutes; the Siren isswitches and off after every 20 seconds automatically;

b) ALL CLEAR: Continuous Blast for two minutes.

All Department Heads and the Designated Personnel are providedwith a Communication Radio to aid in the accountability ofemployees. Therefore, all Department Heads should know theattendance of their employees on any given day to account for theDepartment. If a Department Heads to be absent from work for aperiod of time, they are to transfer the Communication Radio andall associated duties and responsibilities to another actingSupervisor or member of the Safety Committee.

iii. Reliable Measuring Instruments, Control Units and the Servicingof Such Equipment:

Intrinsically safe equipments are used;

Required equipment inter-locks are provided;

Redundant Trips are installed; Emergency Push-Button Trips are provided locally and in the

Control Room; and

All Critical Instruments are provided with Battery back-up.

iv. Precautions in designing of the foundations and load-bearing parts of theBuilding:

Adequate factor of safety has been provided in designing thefoundations of all the Buildings in the factory premises as well as theequipments installed in the plant. The Buildings and the structures areperiodically maintained in tidy condition as per the Building Codes ofPractice.


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v. Continuous Surveillance of operations:

Round the clock surveillance is established in the factory premises,especially in the areas where the fuels such as Coal and Bagasse are

stored in the factory so as to avert any possible untoward incidence.

vi. Maintenance and Repair Work according to the generallyrecognized Rules of good engineering practice;

Electrical maintenance system is streamlined through the check-listscovering preventive maintenance, half-yearly, yearly, turn-around anddaily maintenance for each and every equipment such as motors,switch-gears, batteries, etc. The details of work to be done in each areaare listed and codified.

The Records are computerized, all shut-down works are pre-plannedand requirements of spares are provisioned through the systemiccoordination with the other service and operation departments.

Preventive maintenance in the plant is highly evolved and job-specific.The job history is computerized and the same is used in case of trouble-shooting also. The details about all the equipments are maintained in theareas responsible for such maintenance activities.

vii. Details of Communication facilities available during emergency andthose required for an Off-Site Emergency:

1. Paging system within the factory premises;

2. P & T Telephones; and

3. Walkie-Talkies.


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viii. Details of Fire-Fighting and other facilities available and thoserequired for

an Onff-Site Emergency:

Fire-Fighting Arrangement has been made to ensure completeprotection to the entire factory premises and they broadly include thefollowing:

Sl.

No Category Capacity

Quantity

In Nos1 Dry Chemical Powder Type 70.0kg 2

2 Dry Chemical Powder Type 10.0kg 18

3 Dry Chemical Powder Type 5.0kg 24

4 Carbon-Di-Oxide Type 9.0kg 10






10 Mechanical Foam Type 50ltr 311 Mechanical Foam Type 9ltr 8

12 Trolley Foam Extinguishers 100ltr 5

13 Fire Hose 32

14 Fire Nozzle 14

15 Fire Hydrant Points 47

16 Fire Buckets 70

Fire Pump-House Details:

Fire Pump Motor No.1=Type10UP2:Capacity 200 L/S: Head 22 m; 125 H.P.Fire Pump Motor No.2=Type10UP2:Capacity:200L/S: Head 22 m: 125 H.P.Fire Pump Motor No.3 = Type KPD125/40: 66.2 L/S: Head46 m; 50 H.P.Fire Pump Motor No.4 = Type 6 up 3: Capacity 80 L/S: Head 28 m: 75 H.PFire Pump Motor No.5 = Type 6 up 3: Capacity 80 L/s: Head 28 m: 75 H.PFire Engine = 8 H.P. = One NumberDiesel Generator = 460 K.V.A. Rating.

Fire Water Capacity:

Over-Head Tank Capacity = 9 CUBIC METERS = 2 Nos.Service Water Tank Capacity = 720 CUBIC METERS.


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ix. Details of First-Aid and Hospital Services available and itsadequacy:

One full-time Chief Medical Officer by name, Dr. R. Muthusamy, M.S. and

three other Medical Officers namely Dr. N. Murugan, Dr. A. Vijay Amul Raj

and Dr. A. Hidayathulla are in-charge of the V.M.K. Hospital, Sakthinagar.

Apart from the services of these medical officers to the employees of the

factory and their family members, the following doctors are also engaged on

consultant basis:

1. Dr. R. Balamurugan, M.D.,2. Dr. K. Chinnasamy, M.D.,

3. Dr. G. Ponnusamy, M.S., DNB,

4. Dr. N. Gopisankar, D.O., and

5. Dr. T.J.M. Innocent, M.S., Ortho.

The hospital administration is further strengthened by the services of the

following staffs:

i. Nursing Staff = 18

ii. Dressers = 7

iii. Technicians = 9

iv. Pharmacist = 4

Sufficient number of First-Aid Boxes with trained personnel is provided to

render immediate medical assistance.

The necessary emergency medical services are available from the following

nearby hospitals namely-

a. Government Hospital, Sathy Main Road, Bhavani


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b. Government Hospital, Anthiyur

c. Govarnment Government Hospital, Gobi and

d. Government Hospital, E.V.N. Road, Erode.

e. VMK Hospital, Kav indhapadi.


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Emergency Telephone numbers

Fire Station

S.N

OPLACE & ADDRESS OF

FIRE STATION

RESPONSIBLE

PERSONPHONE NO.

1BHAVANI, NEAR METTURCORNER, METTUR MAINROAD, BHAVANI 638 301

MrR.KRISHNAMOORTHY-SFO

99429-1490304256-230211

2ANTHIYUR, ATHANI MAINROAD, ANTHIYUR 638 501

SFO98421 -1490804256 - 261001

3

GOBINEAR DAILY MARKETKATCHIMEDUSATHI MAIN ROADGOBI -

SFO99429 1490604285 222101

4

ERODEGHANDHI ROADNEAR RAILWAY STATIONERODE - 638 001

DFO

ADDL. DFO

SFO

94425 - 19987,0424 226209994425 - 79930,0424 226209999429 -14901,0424 2267101

5SATHYCOIMBATORE MAIN ROADSATHIYAMANGALAM

SFO99429 - 1490904295 - 220231

Blood Bank:

SL.NO BLOOD BANK CONTACT NOS

1

PERIYAR GOVT. HOSPITAL

E V N ROADERODE

0424 22583550424 2258357

2LOTUS APPOLLO HOSPITAL90, POONDURAI ROAD,ERODE

0424 2282828

3KONGU BLOOD BANKN G G O COLONYERODE

0424 -2271781

4SUBHA CLINIC & BLOOD BANKBROUGH ROADERODE

0424 2258612

5 ERODE BLOOD BANKPATEL STREET 0424 -2253163


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ERODE

6ERODE BLOOD BANKESWARAN KOVIL STREETERODE

0424 2251060

7ARIMA SANGAMERODE

0424 - 2257744

Ambulance

SL.NO. AMBULANCE PHONE NOS.

1. KAVINDAPADI 98658 84280

2. BHAVANI 94430 90690

3.ANTHIYURSPEED AMBULANCESURYA AMBULANCE

98427 -8885694427 - 8000098420 - 53000

4.

ERODELOTUS HOSPITALSENTHIL HOSPITALSAVITHA HOSPITALM M C H

0424 - 22828280424 - 22603750424 - 22503940424 - 2250517

Hospitals

DETAILS OF HOSPITALS.NO

.PLACE AND ADDRESS PHONE NO.

1 SAKTHINAGAR

V M K HOSPITAL 04256 - 246360

2 BHAVANI

GOVERNMENT HOSPITAL 04256 -230333

SAHTY MAIN ROADBHAVANI

3 ANTHIYUR

GOVERNMENT HOSPITAL 04256 - 261350

4 GOBI

GOVERNMENT HOSPITAL 04285 - 222053

ERODE

1 GOVERNMENT HOSPITAL 0424 - 2258355E V N ROAD, ERODE 0424 - 2252356


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0424 - 2252357

2 K M C H 0424 - 2262838

68, PERUNDURAI ROAD, 0424 - 2268244

ERODE

33SENTHIL MULTI SPECIALISTHOSPITAL 0424 - 2260375

PERUNDURAI ROAD, ERODE 0424 - 2260376

4 LOTUS HOSPITAL 0424 - 2282828POONDURAI ROAD,KOLLAMPALAYAM

ERODE

5 SAVITHA 0424 - 2250394BROUGH ROAD, ERODE

C T SCAN CENTRE

JOHNSONS MRI DIAGNOSTIC 0424 - 2262684

426/427 PERUNDURAI ROAD

ERODE

Police Station

DETAILS OF POLICE STATIONS.NO

.PLACE ANDADDRESS

RESPONSIBLE PERSON PHONE NO.

1 SAKTHINAGAR 04256 - 246399

2 BHAVANI D S P 04256 - 230200

04256 - 230243

3 KAVINDAPADI 04256 - 240381

4 ANTHIYUR 04256 - 260250

5 GOBI 04285 - 222041

6 ERODE S P - DISTRICT 0424 - 2258100

S P 0424 - 2260100

0424 - 2261200

D S P 0424 - 2261100

0424 - 2269100

S I 0424 - 2231242

CONTROL ROOM 0424 - 2265100CRIME STOPPERCONTROL 0424 - 2250100

RAILWAY POLICE 0424 - 2255177


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First aid training programme conducted to the employees

THE LIST OF EMPLOYEES ATTENDING THE FIRST AID TRAINING PROGRAMMECONDUCTED BY ST. JOHN AMBULANCE, ERODE

S.NO. EMP.NO NAME DESIGNATION

1 709 P G DURAISAMY SECURITY GUARD2 755 M MUNUSAMY SECURITY GUARD3 5449 P NAGARAJAN WIREMAN - I4 5526 C RAJU OPERATOR - II5 5858 D MANOHARAN ELECTRICIAN6 5529 B N VIJAYAKUMAR OPERATOR - II7 5638 EDWIN D RAJKUMAR ASST BOILER ATTENDANT8 5770 A THANGARASU WELDER - III

9 5839 K ANNADURAI OPERATOR10 5055 K M RAJAGOPAL WIREMAN - I11 5713 A PALANISAMY FITTER - II12 5064 T M MURUGANANDAM WIREMAN - I13 5995 A SUBRAMANIAM ASST FITTER14 5984 K PATTAPPAN ASST FITTER15 5464 K S DURAISAMY ASST FITTER16 5837 M SAKTHIVEL OPERATOR17 5878 N R VENKIDUSAMY EVAPORATE MATE18 5132 K AMARAVATHI FITTER - I19 5865 K RAMARAJ OPERATOR -

PANSTATION

20 5355 P SARAVANAMOORTHY EVAPORATE MATE21 5771 K P ESWARAMOORTHY MACHINIST - II22 5843 P THIRUVENKADAMURUGAN ASST PANMAN23 675 N MURUGESAN SECURITY GUARD

****


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RESPONSIBILITIES AND DUTIES

Duties of the person noticing the emergency

The primary responsibility of informing any emergency situation to the Incident

Controller shall be religiously followed by the person, who notices the fire or Hot

Spots in the Coal Storage Yard of in the factory premises. In turn, the Incident

Controller would consult with the Main Site Controller after having assessed the

emergency situation and declare emergency without any further loss of time. The

Siren will be blown for a longer duration of 2 minutes, at intermission of 15

seconds ON and 5 seconds OFF for 5 times.

The First Responder shall be the vocal alerting system through voice audibility,

pitch, volume and contents of the message. The person who notices the

emergency shall be determined to react and rise up to the occasion through

periodical rehearsals and training. Since the response time to the emergency

scenario is the most critical component of combating the emergencies, his reliable

and specific communication about the nature, magnitude and severity of the

incident shall be clearly shown by his action of carrying the Red Flag hoisted

nearby.

Duties of main site controller

The Main Site Controller shall have the control options/in his absence, the

alternate Main Site Controller or the Incident Controller shall have the scenario

analysis/ to initiate LEVEL I, LEVEL II OR LEVEL III Emergencies:

Level I Emergency:

Minor Emergency managed by Department level.

Level II Emergency;

Possible Emergencies like Fire or Hazardous Chemical Spillage that can be

controlled by the Factory Level.

Level III Emergency:


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Major Emergency like Fire/Explosion that could affect the environment, where

outside help from the Tamilnadu Fire and Rescue Service is required.

The Site Main Controller/Incident Controller shall be able to demonstrate:

How to implement the On-Site Emergency Plan;

How to implement the command system;

How to identify, to the extent possible, all credible accident scenarios or the

conditions present;

How to address the Site Analysis, use of Engineering Controls, Hazardous

Materials Handling Procedures and use of new techniques; How to determine- through monitoring, when personnel protective

equipments or respiratory protection is required;

How to give training to the First Responders based on their duties and

functions within the factory premises; the skill and training required for all

new Responders shall be conveyed to them through training, before they are

permitted to take part in the actual Emergency Situation;


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A First Responder Awareness Level Employee is an individual who is likely

to witness or discover a hazard and who, through training, is expected to

initiate a response system by notifying the appropriate authorities of thefire/hazardous material spillage. They are not expected to take further action;

A First Responder Operation Level Employee is an individual who is

expected to respond to the fire scenario as part of initial action to protect

nearby personnel, property or the environment from the effects of fire. They

are trained to respond defensively to the fire scenario without necessarily

being expected to extinguish the fire;

They shall have the knowledge of hazards and the risks associated with

employees wearing the personal protective clothing;

How to decontaminate the spill of corrosive chemicals such as molasses,

caustic lye, Hydrochloric Acid, etc.;

When to determine for termination procedures; and

They shall also be familiar with the additi onal details of Dust Explosions:

1. For an explosion to occur a gas cloud with a concentration

between Upper Flammability Limit (UFL) and Lower Flammability

Limit (LFL) must be ignited. The over-pressure caused by the

explosion would depend, among other things, on:

i) The gas or gas mixture present;

ii) The cloud volume and concentration;

iii) Ignition source type and location;

iv) The confinement or venting surrounding the gas cloud;


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v) The congestion or obstacle within the cloud (size,

shape, number, location); and

vi) Ignition timing.

Gas explosions in more open environments can also lead to significant over-

pressures depending on the rate of combustion and the mode of flame

propagation in the cloud. All of the above points from (i) to (vi) can affect the

explosion.

Duties of technical officer

The Technical Officer shall be able to demonstrate the implementation of the

Emergency Response Plan;

The knowledge of the classification, identification and verification of known

and unknown materials by using field survey instruments and equipments

shall be acquired;

Ability to function within the assigned role in the incident command system

shall be exercised;

The knowledge of the selecting and using proper specialized chemical

protective equipments shall be executed;

The knowledge of in-depth Hazard and Risk Assessment Techniques shall

be possessed;

Notification to the Incident Controller without any further loss of time has a

great significance in view of the following toxic effects of Carbon Monoxide:


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CO in Air in % Volume.Symptoms0.1 No symptoms- No damage0.2 Mild head-ache; few other

symptoms.

0.04 Head-ache up to 1 to 2 Hours.0.08 Head-ache up to 45 minutes;

Nausea, collapse, unconsciousafter one Hour.

0.10 Dangerous- unconscious after One Hour

0.16 Head-ache, dizziness, nauseaafter 20 minutes.

0.32 Head-ache, dizziness, nauseaafter 5 to 10 minutes; unconsciousafter 30 minutes.

0.64 Head-ache, dizziness, nauseaafter 1 to 2 minutes; unconsciousafter 10 to 15 minutes;

1.26 Immediate unconsciousness;Danger of death in 1 to 3 minutes.

Performance of advance control, containment and confinement operations

within the capabilities of the resources available shall be secured;

Understanding of the implementation of decontamination procedures shall be

arrived;

Understanding of the basic chemical and toxicological terminology shall be

infused; and

Understanding of the termination procedures shall be propagated.


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Duties of the fire fighting officer

Identification of the standard fire fighting functions or evaluations expected of them

based on the emergency scenario to be assigned, including functions or

evaluations shall be performed simultaneously. T he specific Fire-Safety Rules,

Procedures and First-Aid/Medical Attention Services shall be performed according

to the type of each emergency incident.

Whenever any Hot Work Operations are essential in the course of emergency

activities, the following SIX STEP RULES shall be adhered to in interest of safety:

1. Conduct safety meeting with other officers;

2. Put up Warning Sign at the site;

3. Move combustibles away from the Hot Work site;

4. Shield combustibles with fire blankets or Welder blankets;

5. Provide fire watch; have nearby appropriate fire extinguisher and telephone

and evacuate the area, if the fire could not be extinguished immediately;

6. Protect stored materials with thermal barrier such as half an inch gypsum

board as soon possible.

Effective communications ensures that the fire-fighting crew understands their

responsibilities during an assigned task. Effective coordination prevents conflicting

activities and ensures that a proper sequence is followed, while conducting an

assigned task. This becomes increasingly important, as more agencies such as

Tamilnadu Fire and Rescue Service and mutual aid member would be involved in

mitigation activities. Written code of practice shall be observed during fire-fighting

by each and everyone of the crew .,

It is not necessary to develop standard operating procedures regarding every

possible exposure to Carbon-Monoxide and Carbon-Di-Oxide atmospheres in the

course of fire-fighting activities. What is expected is the procedures would be

followed by way of wearing personal protective equipments, which is mandatory

for their own protection.


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Apart from the active fire-fighting crew, the Incident Controller and the Fire-

Fighting Officer shall wear personal protective equipments invariably. Fit Testing

shall be conducted for one and all the fire-fighting crew and the equipments shall

be made available in the correct size.

Duties of the communication officer

Emergency Communications and Warning Protocols, process and

procedures shall be developed, periodically tested and used to alert people

potentially impacted by an actual or impending emergency;

The Communication Officer shall develop procedures to disseminate and

respond to requests for pre-disaster, disaster and post-disaster information

including procedures to provide information to the Media and other external

audience and deal with their enquiries.

Effective Radio Communication shall be ensured in the interest of safety;

The channel shall be monitored before transmitting;

The message shall be planned suitably before pushing the transmitter

switch;

The push-to talk button in the Radio shall be pressed first and then wait for

one second before starting the message, otherwise the first part of the

message would be cut off due to the transmitter to work at its full power;

The micro-phone shall be held two inches away from the mouth;

The unit or person shall be first identified;

The message transmitted shall be acknowledges as soon as possible bysaying GO AHEAD. If long messages could not be taken for some

reasons, simply STANDBY shall be recorded until the problem is solved;

While transmitting a number with two or more digits, first the entire number

shall be given and then each digit separately; for example, the number

sixty three shall be recorded as 63 first and then SIX and THREE shall

be followed;

Exclusive frequency shall be ensured for Emergency Management Services

and the back-ground noise shall be as much as possible;


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There shall be adequate and proper communication from each stage of a

plan to the next, so that the Hazard Management Decisions could be

understood, recorded and audible. One way of achieving this is by

summarizing the key information of fire and explosion events in the factorypremises; and

The summary of the key information shall be a living document which in its

simplest form may be a compilation of entire details. It should convey

information to all those who are responsible for operations in full, which is in

concise and easily read.

Duties of the rescue officer

Because air-way maintenance is one of the very important skills that has to

be learn by the Rescue Team Members and also the respiratory system

shall be the first of the body systems to be reviewed in the course of an

emergency;

Unconscious persons who have not suffered trauma shall be placed in a

side-laying or RECOVERY POSITION to help keep air-way open;

Improperly lifting or moving a person can result in injury to either the

responder or to the injured person. By exercising Good Body Mechanics,

the possibility of injuring self as well as the injured would be reduced. Good

Body Mechanics means using the strength in the large muscles from the

legs to lift a person instead of applying back muscles;

To lift safely, the Rescue Crew shall keep certain guide-lines in mind.

Before attempting to move a person, check the weight of the patient; if

required another person may be called for the help. The rescue work shall

be carried out in an efficient and helpful; manner;

If the patient is on the floor or on the ground during an emergency situation,

the Rescue Team Members may have to drag the person away from the

site instead of trying to lift them and carry. Every effort shall be made to pull

the person in the direction of long axis of the body in order to provide as


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much spinal protection for the person as possible. This sort of CLOTHES

DRAGGING is the simplest way to move a person in an emergency;

If the person is clothed in dress that could tear away easily during clothes

drag (foe example, burnt partially) the person injured shall be moved byusing a blanket or large bed-sheet, which is termed as BLANKET DRAG;

If any large sheet is not readily available, the injured person shall be carried

by ARMS TO ARMS DRAG by placing the hands under the lying person

s arm-pits from the back of the person and grasping the persons

fore-arm;

There shall be close coordination and effective communication between the

Rescue Team and the Rehabilitation Team; and

The Rescue Officer shall also hold responsibility for the shutting down the

critical plants in the course of their emergency rescue operations in the

factory premises.

Duties of the rehabilitation officer

The Rehabilitation Officer shall establish logical capability and the

procedures to locate, store, distribute, maintain, test and account for

services, personnel , resource materials and facilities procured for the

purpose of supporting the Emergency Plan;

Procedures shall include, but not limited to, the following:

1. Control of access to the area affected by the emergency;

2. Identification of personnel engaged in Emergency Activities at the

scene of accident;

3. Accounting for the personnel engaged in various activities;

4. Accounting for the personnel affected, displaced or injured by the

incident;

5. Mobilization and Demobilization of the resources;

6. Provision of temporary, short-term or long-term shelters, feeding and

care of people displaced by the emergency;

7. Recovery, identification and safe-guarding of human remains;


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8. Provision of mental health and physical well-being of the individuals

affected by the emergency;

9. Provision for managing the critical incident stress of the Responders;

and

10. The Rehabilitation Officer shall develop functional administrative

procedures to support the entire sequence of operations like pre-

disaster, disaster and post-disaster scenarios.


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Duties of the employees

1. The employees in the factory including contractors and their contract

workers shall, to the extent to which they are expected, that is, within their

competency and skills, shall comply with all procedures and protection

relating to the prevention and control of Major Accidents within the factory

premises;

2. They shall comply with all emergency procedures, should a Major Accident

or Near Miss Accident occur;

3. They shall report promptly to the Incident Controller/Shift-in-Charge any

matter of which they are aware that they may affect the facility compliance;

4. They shall take, within the scope of their job, and without being placed at

any disadvantage, corrective action and, if necessary, interrupt the

operations/processes of the factory. Where on the basis of their training and

skills, they have responsible jurisdiction to believe that there is an imminent

danger of a Major Accident and notify to the Incident Controller/Shift-in-

Charge or raise an alarm, as appropriate, before or, as far as possible, after

taking such action;

5. They shall discuss with the Emergency Coordinating Officers any potential

hazards that they consider are capable of generating a Major Accident and

they also have the Right to notify the relevant District Administration

Authorities of those hazards and

6. They shall also be consulted through appropriate consultative mechanism in

order to provide the Safe System of Work in and around the factory

premises.

****


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PRESIDENT - SAKTHINAGAR

CANE DEPARTMENT ADMINISTRATIVE DEPARTMEN

ENGINEERING DEPARTMENT MANUFACTURING DEPARTMENTDISTILLERY DEPARTM


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Page: 47 of 50

ADMINISTRATIVE DEPARTMENT

DY. GENERAL MANAGER - ADMIN ASST. GEN. MANAGER - HRD

ASST. GEN. MANAGE

ACCOUNTS

H R D OFFICE

STAFFS - TIME OFF

SECURITY

CANE ACCOU

MAIN ACCOU

GUEST HOUSE &TELEPHONE

DRIVERS & MECHANICDY. MANAG

ACCOUNT

SR. OFFICE

CANE ACCOU

ACCOUSTAFFS

ACCOUNTS

STAFFS

Sr. Off. -L.

A. S. O.

MANAGER -

SYSTEMS

STAFFS - SYSTEMS

ENGINEER- AUTOMOBILE


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Page: 48 of 50

ASST GEN MANAGER - ENGINEERING

MECHANICAL

WORKER

ENGINEERING DEPARTMENT

ELECTRICAL

SHIFT-ENGINEER

SHIFT-ENGINEER

MANAGER MECHANICAL

WORKER ELECTRICIAN

MANAGER

MECHANICAL

MANAGER -ELECTERICAL

SHIFT-ENGINEER

CO-GENMAIN STO

ASST

MANAGE

STORE - STA

ASSTMANAG

CIVIL

ENGINECIVIL

DY GENERAL MANAGER - PROCE

SR. MANAGER - PROCESS

SHIFT - CHEMIST

MANUFACTURING DEPARTMENT

LAB-IN-CHARGE

WORKER

ASST. MANAGER-

GODOWNGODOWN STAFFLABOURERS

SHIFT - CHEWORKER


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MANAGER - PROCESS

LAB CHEMIST

MANAGER

WATER TREATME


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**** ****

WORKER

DEPUTY MANAGER

DY. GENERAL MANAGER - DISTILL

SHIFT CHEMIST

DISTILLERYCANE DEPARTMENT

GENERAL MANAGER - CANE

ASST. GEN. MANAGER - CANE

MANAGER CANE

CANE OFFICERS -DIVISION

HEADS

SUPERVISOR- YARD &TRANSPORT

WEIGHBRIDGE

OPERATORWEIGHBRIDG

CAME INSPECTORS- SECTION IN-

CHARGE

Bannariamman Onsite

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